首页> 外国专利> INTEGRATED CONTINUOUS CONVERSION AND SEPARATION METHODS FOR UPCYCLING MIXED PLASTIC WASTE TO CLEAN GASOLINE AND DIESEL FUELS AND OTHER PRODUCTS

INTEGRATED CONTINUOUS CONVERSION AND SEPARATION METHODS FOR UPCYCLING MIXED PLASTIC WASTE TO CLEAN GASOLINE AND DIESEL FUELS AND OTHER PRODUCTS

机译:将升高混合塑料废料的综合连续转换和分离方法,以清洁汽油和柴油燃料等产品

摘要

A method of producing useful fuel fluids from solid plastic waste, including loading solid plastic waste matter into a reaction chamber to define a load, subjecting the load to HTP to extract hydrocarbon mixtures, filtering the hydrocarbon mixtures to extract solid matter, and separating the hydrocarbon mixtures into a light fraction (C1 to C25) and a heavy fraction (C26 to C31). The heavy fraction is directed to a first container and the light fraction is directed to a second container. The light fraction is separated into diesel (C8-C25), gasoline (C4-C12), and vapor (C1-C5), and the diesel is directed to a third container, the gasoline is directed to a fourth container, and the vapor is directed to a fifth container. The hydrocarbon mixtures have a carbon number distribution between C1 and C31. The pressure in the reaction chamber is typically between 0.1 and 10 MPa and the temperature in the reaction chamber is between 350 and 500 degrees Celsius. The plastic waste is selected from the group consisting of PS, PE, PP, and mixtures thereof.
机译:一种从固体塑料废物生产有用的燃料流体的方法,包括将固体塑料废物物加入反应室以限定负荷,使负荷对HTP进行萃取烃混合物,过滤烃混合物以提取固体物质,并分离烃并分离烃。将混合物混合成光级分(C1至C25)和重级分(C26至C31)。重馏分涉及第一容器,并且光部分涉及第二容器。将光级分分离成柴油(C8-C25),汽油(C4-C12)和蒸气(C1-C5),并且柴油涉及第三容器,汽油涉及第四容器,汽油被引导到第五容器。烃混合物在C1和C31之间具有碳数分布。反应室中的压力通常在0.1和10MPa之间,反应室中的温度在350至500摄氏度之间。塑料废物选自PS,PE,PP及其混合物。

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